US8322161B2 - Process and apparatus for producing glass sheet - Google Patents
Process and apparatus for producing glass sheet Download PDFInfo
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- US8322161B2 US8322161B2 US12/810,173 US81017308A US8322161B2 US 8322161 B2 US8322161 B2 US 8322161B2 US 81017308 A US81017308 A US 81017308A US 8322161 B2 US8322161 B2 US 8322161B2
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- glass
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- glass sheet
- cooling chamber
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- 239000011521 glass Substances 0.000 title claims abstract description 225
- 238000000034 method Methods 0.000 title claims abstract description 32
- 238000001816 cooling Methods 0.000 claims abstract description 66
- 238000000137 annealing Methods 0.000 claims abstract description 63
- 239000006060 molten glass Substances 0.000 claims abstract description 37
- 238000003280 down draw process Methods 0.000 claims abstract description 22
- 238000005520 cutting process Methods 0.000 claims abstract description 20
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 18
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 claims description 16
- 229910052906 cristobalite Inorganic materials 0.000 claims description 10
- 238000007500 overflow downdraw method Methods 0.000 claims description 10
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 9
- 229910052593 corundum Inorganic materials 0.000 claims description 9
- 229910001845 yogo sapphire Inorganic materials 0.000 claims description 9
- 229910052681 coesite Inorganic materials 0.000 claims description 8
- 239000000377 silicon dioxide Substances 0.000 claims description 8
- 229910052682 stishovite Inorganic materials 0.000 claims description 8
- 229910052905 tridymite Inorganic materials 0.000 claims description 8
- 239000006025 fining agent Substances 0.000 claims description 6
- 239000004973 liquid crystal related substance Substances 0.000 description 12
- 230000000694 effects Effects 0.000 description 8
- 238000004519 manufacturing process Methods 0.000 description 8
- KRHYYFGTRYWZRS-UHFFFAOYSA-N hydrofluoric acid Substances F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 description 7
- GOLCXWYRSKYTSP-UHFFFAOYSA-N Arsenious Acid Chemical compound O1[As]2O[As]1O2 GOLCXWYRSKYTSP-UHFFFAOYSA-N 0.000 description 6
- 229960002050 hydrofluoric acid Drugs 0.000 description 6
- 230000003449 preventive effect Effects 0.000 description 6
- 230000015572 biosynthetic process Effects 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- XOLBLPGZBRYERU-UHFFFAOYSA-N tin dioxide Chemical compound O=[Sn]=O XOLBLPGZBRYERU-UHFFFAOYSA-N 0.000 description 4
- 239000002253 acid Substances 0.000 description 3
- 229910000272 alkali metal oxide Inorganic materials 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- ADCOVFLJGNWWNZ-UHFFFAOYSA-N antimony trioxide Inorganic materials O=[Sb]O[Sb]=O ADCOVFLJGNWWNZ-UHFFFAOYSA-N 0.000 description 2
- 230000008602 contraction Effects 0.000 description 2
- 230000003028 elevating effect Effects 0.000 description 2
- 230000002708 enhancing effect Effects 0.000 description 2
- 239000005357 flat glass Substances 0.000 description 2
- 230000002093 peripheral effect Effects 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 239000000758 substrate Substances 0.000 description 2
- YEAUATLBSVJFOY-UHFFFAOYSA-N tetraantimony hexaoxide Chemical compound O1[Sb](O2)O[Sb]3O[Sb]1O[Sb]2O3 YEAUATLBSVJFOY-UHFFFAOYSA-N 0.000 description 2
- DLYUQMMRRRQYAE-UHFFFAOYSA-N tetraphosphorus decaoxide Chemical compound O1P(O2)(=O)OP3(=O)OP1(=O)OP2(=O)O3 DLYUQMMRRRQYAE-UHFFFAOYSA-N 0.000 description 2
- FUJCRWPEOMXPAD-UHFFFAOYSA-N Li2O Inorganic materials [Li+].[Li+].[O-2] FUJCRWPEOMXPAD-UHFFFAOYSA-N 0.000 description 1
- KKCBUQHMOMHUOY-UHFFFAOYSA-N Na2O Inorganic materials [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 description 1
- 229910019714 Nb2O3 Inorganic materials 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- GHPGOEFPKIHBNM-UHFFFAOYSA-N antimony(3+);oxygen(2-) Chemical compound [O-2].[O-2].[O-2].[Sb+3].[Sb+3] GHPGOEFPKIHBNM-UHFFFAOYSA-N 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 230000009194 climbing Effects 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- XUCJHNOBJLKZNU-UHFFFAOYSA-M dilithium;hydroxide Chemical compound [Li+].[Li+].[OH-] XUCJHNOBJLKZNU-UHFFFAOYSA-M 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000005401 electroluminescence Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000010408 film Substances 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 238000005305 interferometry Methods 0.000 description 1
- MRELNEQAGSRDBK-UHFFFAOYSA-N lanthanum oxide Inorganic materials [O-2].[O-2].[O-2].[La+3].[La+3] MRELNEQAGSRDBK-UHFFFAOYSA-N 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- KTUFCUMIWABKDW-UHFFFAOYSA-N oxo(oxolanthaniooxy)lanthanum Chemical compound O=[La]O[La]=O KTUFCUMIWABKDW-UHFFFAOYSA-N 0.000 description 1
- 238000005498 polishing Methods 0.000 description 1
- NOTVAPJNGZMVSD-UHFFFAOYSA-N potassium monoxide Inorganic materials [K]O[K] NOTVAPJNGZMVSD-UHFFFAOYSA-N 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- AKEJUJNQAAGONA-UHFFFAOYSA-N sulfur trioxide Inorganic materials O=S(=O)=O AKEJUJNQAAGONA-UHFFFAOYSA-N 0.000 description 1
- 230000001629 suppression Effects 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
- RUDFQVOCFDJEEF-UHFFFAOYSA-N yttrium(III) oxide Inorganic materials [O-2].[O-2].[O-2].[Y+3].[Y+3] RUDFQVOCFDJEEF-UHFFFAOYSA-N 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B17/00—Forming molten glass by flowing-out, pushing-out, extruding or drawing downwardly or laterally from forming slits or by overflowing over lips
- C03B17/06—Forming glass sheets
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/50—Glass production, e.g. reusing waste heat during processing or shaping
- Y02P40/57—Improving the yield, e-g- reduction of reject rates
Definitions
- the present invention relates to a process and apparatus for producing a glass sheet, the process involving causing a molten glass to flow down from a forming trough, and vertically down-drawing a glass ribbon.
- a process for producing a glass sheet for various electronic instruments in particular, a flat panel display such as a liquid crystal display
- a down-draw method in which a glass sheet is produced by causing a molten glass to flow down from a forming trough, and vertically down-drawing a glass ribbon.
- the down-draw method includes two methods, i.e., an overflow down-draw method and a slot down-draw method.
- the overflow down-draw method is widely known as a method, with which a glass sheet having very small waviness and roughness on its surface and being excellent in surface quality can be obtained.
- the overflow down-draw method is a method, which involves continuously feeding a molten glass to a top portion of a forming trough having a wedge-shaped cross-section, causing the molten glass to flow down from the top portion of the forming trough along both side surfaces of the forming trough, and allowing the molten glasses to fuse at a lower end portion of the forming trough to form a sheet-like glass ribbon, and causing the glass ribbon to flow down through a conveyance passage extending vertically while holding the glass ribbon at both edge portions with a plurality of pulling rollers, thereby down-drawing the molten glass into a glass ribbon.
- the glass ribbon is gradually solidified, and a glass sheet having a given width and thickness is obtained. Further, atmospheric temperature in the conveyance passage is strictly controlled, and the internal strain (thermal strain) in the glass sheet is sufficiently reduced thereby. Then, the glass sheet is cooled to around room temperature.
- JP-A-5-124826 discloses a structure including supporting a roller on a single side for preventing occurrence of an internal strain in a glass sheet caused by the influence of the cooling of a roller shaft so as to prevent the deformation of the glass sheet, and also discloses a preventive plate against convection for separating a conveyance passage horizontally for preventing the internal strain in a glass ribbon caused by thermal convection occurring in the conveyance passage.
- JP-A-10-53426 discloses a process for producing a glass sheet having a small internal strain, the process involving forming a plurality of chambers by separating an internal space of a forming furnace or an annealing furnace horizontally, and allowing each chamber to have a room temperature-controlling function to carry out sufficient annealing.
- JP-A-2001-31435 discloses a technology by which temperature distribution in the annealing furnace is also formed in a width direction of a glass ribbon, to thereby prevent a minute internal strain or deformation.
- a glass sheet used for the liquid crystal display In recent years, high definition and high quality are increasingly demanded for a liquid crystal display, and it is demanded for a glass sheet used for the liquid crystal display to have a maximum value of an internal strain of 1.0 MPa or less. Further, a glass sheet for a liquid crystal display is rapidly moving toward a large-size plate. For example, even a glass ribbon having a width of 2000 mm or more as the width size of a portion serving as a final glass product (effective width) is produced. However, as the size of a glass sheet produced is becoming larger, an internal strain in the glass sheet also tends to become larger, and hence it is becoming difficult to control the internal strain to 1.0 MPa or less.
- low-temperature airflow One of the causes for the internal strain in a glass sheet is flow of air climbing along the surface of a glass ribbon (hereinafter referred to as low-temperature airflow). That is, in a conveyance passage of a glass ribbon, low-temperature airflow always climbs along the surface of the glass ribbon, causing easy variation of the atmospheric temperature in an annealing furnace.
- JP-A-5-139766 discloses formation of a preventive plate against convection in an annealing furnace, but because low-temperature airflow climbs near the surface of a glass ribbon, the preventive plate against convection cannot cut off the low-temperature airflow sufficiently.
- a technological object of the present invention is to provide a process for obtaining a glass sheet of high quality with good productivity by avoiding a problem with an internal strain that becomes serious as the move toward a large-size glass sheet progresses.
- the inventors of the present invention have made various studies to solve the above-mentioned problem. As a result, the inventors have found that the climb of low-temperature airflow can be suppressed in the conveyance passage of a glass ribbon by providing a cooling chamber with a gas exhausting passage, thereby reducing the amount of the low-temperature airflow flowing from the cooling chamber to the annealing furnace. Thus, the present invention has been proposed.
- a first aspect of the invention made for solving the above-mentioned problem relates to a process for producing a glass sheet including: a forming step of down-drawing a molten glass into a sheet-like glass ribbon, in which the molten glass is fed to a forming trough arranged in a forming furnace and the molten glass is caused to flow down from the forming trough through a conveyance passage extending vertically; an annealing step of removing an internal strain in the glass ribbon in an annealing furnace; a cooling step of cooling the glass ribbon to around room temperature; and a cutting step of cutting the glass ribbon in a given size, in which the cooling chamber is provided with a gas exhausting passage, thereby exhausting air in the cooling chamber to an outside.
- a second aspect of the invention made for solving the above-mentioned problem relates to the process for producing a glass sheet according to the first aspect further including exhausting the air in the cooling chamber into a chamber surrounding a forming furnace and/or an annealing furnace through the gas exhausting passage.
- a third aspect of the invention made for solving the above-mentioned problem relates to the process for producing a glass sheet according to the first or second aspect, in which the forming step includes a step of forming a glass ribbon by an overflow down-draw method or a slot down-draw method.
- a fourth aspect of the invention made for solving the above-mentioned problem relates to the process for producing a glass sheet according to any one the first to third aspects, in which a length of a short side of the glass sheet is 2000 mm or more.
- a fifth aspect of the invention made for solving the above-mentioned problem relates to the process for producing a glass sheet according to any one of the first to fourth aspects, in which a maximum value of the internal strain of the glass sheet is 1.0 MPa or less.
- a sixth aspect of the invention made for solving the above-mentioned problem relates to the process for producing a glass sheet according to any one of the first to fifth aspects, in which the glass sheet contains, in terms of mass %, 40 to 70% of SiO 2 , 2 to 25% of Al 2 O 3 , 0 to 20% of B 2 O 3 , 0 to 10% of MgO, 0 to 15% of CaO, 0 to 10% of SrO, 0 to 15% of BaO, 0 to 10% of ZnO, 0 to 10% of ZrO 2 , and 0 to 2% of an fining agent.
- a seventh aspect of the invention made for solving the above-mentioned problem relates to an apparatus for producing a glass sheet including: a forming furnace for down-drawing a molten glass into a sheet-like glass ribbon, in which the molten glass is fed to a forming trough and the molten glass is caused to flow down from the forming trough through a conveyance passage extending vertically; an annealing furnace for removing an internal strain in the glass ribbon; a cooling chamber for cooling the glass ribbon to around room temperature; and a cutting chamber for cutting the glass ribbon in a given size, in which the cooling chamber is provided with a gas exhausting passage.
- An eighth aspect of the invention made for solving the above-mentioned problem relates to the apparatus for producing a glass sheet according to the seventh aspect, in which the gas exhausting passage of the cooling chamber is communicated with a chamber surrounding a forming furnace and/or an annealing furnace.
- the invention according to the first aspect provides the cooling chamber with a gas exhausting passage to exhaust the air in the cooling chamber to the outside, to thereby allow the air in the cooling chamber to be exhausted while being dispersed into both of the conveyance passage of the glass ribbon and the gas exhausting passage, with the result that the climb of low-temperature airflow can be suppressed in the conveyance passage.
- the cooling chamber is preferably provided with the gas exhausting passage at its ceiling portion because the air-exhausting effect becomes larger.
- the invention according to the second aspect allows the air in the cooling chamber to be exhausted to a chamber surrounding a forming furnace and/or an annealing furnace through the gas exhausting passage, to thereby elevate the pressure in the chamber surrounding a forming furnace and/or an annealing furnace.
- an effect of suppressing the climb of the low-temperature airflow in the conveyance passage of the glass ribbon becomes larger. That is, the low-temperature airflow that has climbed from the cooling chamber into the annealing furnace is heated in the annealing furnace, and then part of the low-temperature airflow leaks into the outside atmosphere through the gaps of furnace walls of the forming furnace and/or an annealing furnace.
- the elevation of the pressure in the chamber surrounding a forming furnace and/or an annealing furnace suppresses the leakage of the inside air of the forming furnace and/or annealing furnace.
- the effect of suppressing the climb of the low-temperature airflow in the conveyance passage of the glass ribbon becomes larger.
- the forming step is a step for forming a glass ribbon by an overflow down-draw method or a slot down-draw method and hence a thin plate glass can be efficiently formed.
- the overflow down-draw method is a method involving supplying a molten glass to a forming trough having an aperture in a long-hole shape (slot shape), then pulling the molten glass out of the aperture of the forming trough to form a sheet-like glass ribbon, and vertically extending and forming the glass ribbon into a glass sheet.
- the glass ribbon flowing down vertically may be cut in the width direction of the glass ribbon (direction perpendicular to the flowing-down direction of the glass ribbon) from the cooling step, or the glass ribbon may be bent from the vertical direction to the horizontal direction and cut in the width direction while being moved in the horizontal direction.
- the glass sheet has a length of the short side of 2000 mm or more, and hence many glass sheets for a display panel can be cut out from one piece of the glass sheet (original sheet), enabling the improvement in the production efficiency.
- the larger the size of the glass sheet the larger the internal strain of the glass sheet tends to be.
- the apparatus for producing a glass sheet has to be larger, resulting in the easiness for low-temperature air to flow in the conveyance passage of the glass ribbon, with the result that the variation of the atmospheric temperature in the annealing furnace easily occurs.
- the present invention becomes useful when the invention is used for producing particularly large glass sheets, specifically, a glass sheet having a length of the short side of 2000 mm or more, preferably 2500 mm or more, or still more preferably 3000 mm or more.
- the glass sheet has a maximum value of an internal strain of 1.0 MPa or less, and hence the image of a liquid crystal display is prevented from becoming nonuniform due to birefringence.
- the variation of the atmospheric temperature in the annealing furnace can be suppressed to a minimum extent, leading to the suppression of the internal strain in the glass sheet even if the size of the glass sheet becomes large.
- the glass sheet contains, in terms of mass %, 40 to 70% of SiO 2 , 2 to 25% of Al 2 O 3 , 0 to 20% of B 2 O 3 , 0 to 10% of MgO, 0 to 15% of CaO, 0 to 10% of SrO, 0 to 15% of BaO, 0 to 10% of ZnO, 0 to 10% of ZrO 2 , and 0 to 2% of a fining agent, and hence the glass sheet satisfies characteristics such as chemical resistance (good acid resistance, good alkali resistance, and good buffered-hydrofluoric-acid resistance), thermal resistance (strain point of 630° C.
- meltability (1600° C., temperature corresponding to a viscosity of 10 2.5 poise)
- formability liquidus temperature of 1150° C. or less
- thermal expansion coefficient 25 to 45 ⁇ 10 ⁇ 7 /° C. at a temperature of 30 to 380° C.
- SiO 2 is a component for forming the network of glass and has effects of reducing the thermal expansion coefficient of glass, making the internal strain smaller, improving the acid resistance of glass, and elevating the strain point of glass to make the thermal contraction of a glass sheet smaller.
- the content of SiO 2 is 40 to 70%, preferably 50 to 67%, or more preferably 57 to 64%.
- Al 2 O 3 is a component for reducing the thermal expansion coefficient of glass and for making the internal strain of a glass sheet smaller. Further, Al 2 O 3 has effects of elevating the strain point of glass and suppressing the precipitation of devitrified stones of cristobalite as well. However, when the content of Al 2 O 3 becomes large, the buffered-hydrofluoric-acid resistance of glass deteriorates and liquidus temperature rises, resulting in a difficulty in formation. Thus, the content of Al 2 O 3 is 2 to 25%, preferably 10 to 20%, or more preferably 14 to 17%.
- B 2 O 3 is a component, acting as a melting accelerate component, for reducing the viscosity of glass and for improving the meltability. Further, B 2 O 3 is a component for reducing the thermal expansion coefficient of glass and for making the internal strain of a glass sheet smaller. However, when the content of B 2 O 3 becomes large, the strain point of glass easily lowers and the acid resistance easily deteriorates. Thus, the content of B 2 O 3 is 0 to 20%, preferably 5 to 15%, or more preferably 7.5 to 12%.
- MgO is a component for improving the meltability of glass by reducing only the viscosity of the glass without reducing the strain point.
- the content of MgO becomes large, devitrified stones easily precipitate in glass, and buffered-hydrofluoric-acid resistance lowers, with the result that when a glass sheet is treated with a buffered hydrofluoric acid, the surface of the glass sheet is corroded, a reaction product attaches to the surface, and the surface easily becomes clouded.
- the content of MgO is 0 to 10%, preferably 0 to 5%, or more preferably 0 to 3.5%.
- CaO is a component for improving the meltability of glass by reducing only the viscosity of the glass without reducing the strain point.
- the content of CaO becomes large, buffered-hydrofluoric-acid resistance easily deteriorates.
- the content of CaO is 0 to 15%, preferably 0 to 12%, or more preferably 3.5 to 9%.
- SrO is a component for enhancing the chemical resistance and denitrification resistance of glass.
- the content of SrO becomes large, the thermal expansion coefficient of glass easily becomes large and the internal strain of a glass sheet tends to become large.
- the content of SrO is 0 to 10%, preferably 0 to 8%, or more preferably more than 0.5 to 8%.
- BaO is a component for enhancing the chemical resistance and denitrification resistance of glass similar to SrO.
- the content of BaO is 0 to 15%, preferably 0 to 10%, or more preferably 0 to 8%.
- ZnO is a component for improving the buffered-hydrofluoric-acid resistance and meltability of glass.
- the content of ZnO becomes large, the denitrification resistance and strain point of glass easily lowers.
- the content of ZnO is 0 to 10%, preferably 0 to 5%, or more preferably 0 to 1%.
- ZrO 2 is a component for raising the strain point of glass.
- the content of ZrO 2 becomes large, the density of glass remarkably increases, and devitrified stones derived from ZrO 2 easily precipitate.
- the content of ZrO 2 is 0 to 10%, preferably 0 to 7%, or more preferably 0 to 5%.
- As 2 O 3 , Sb 2 O 3 , SnO 2 , SO 3 , F, Cl, or the like can be used as a fining agent up to 2%. It should be noted that the use of As 2 O 3 and Sb 2 O 3 should be avoided because they are environmental load substances, and when the use of As 2 O 3 and Sb 2 O 3 is avoided, SnO 2 is contained preferably at 0.01 to 2%.
- R 2 O alkali metal oxides
- Na 2 O, K 2 O, and Li 2 O should not be contained because when those components are contained, the characteristics of various films and TFT devices formed on the glass sheet for a liquid crystal display may be degraded.
- the content in terms of R 20 must be regulated at 0.1% or less.
- an apparatus for producing a glass sheet includes a forming furnace for down-drawing a molten glass into a sheet-like glass ribbon, in which the molten glass is fed to a forming trough and the molten glass is caused to flow down from the forming trough through a conveyance passage extending vertically, an annealing furnace for removing an internal strain in the glass ribbon; a cooling chamber for cooling the glass ribbon to around room temperature; and a cutting chamber for cutting the glass ribbon in a given size, the cooling chamber being provided with a gas exhausting passage to exhaust the air in the cooling chamber to the outside, to thereby allow the air in the cooling chamber to be exhausted while being dispersed into both of the conveyance passage of the glass ribbon and the gas exhausting passage, with the result that the climb of low-temperature airflow can be suppressed in the conveyance passage.
- the variation of the atmospheric temperature in the annealing furnace can be suppressed to a minimum extent, leading to
- the gas exhausting passage of the cooling chamber is communicated with the chamber surrounding a forming furnace and/or an annealing furnace, the air in the cooling chamber is allowed to flow into the chamber surrounding a forming furnace and/or an annealing furnace, causing the elevation of the pressure in the chamber, to thereby provide a rare possibility for the inside air in the forming furnace and/or annealing furnace to leak into the outside through the gaps of furnace walls of the furnaces.
- an effect of suppressing the climb of the low-temperature airflow in the conveyance passage of the glass ribbon becomes larger.
- FIG. 1 is a schematic front view illustrating an apparatus for producing a glass sheet of the present invention.
- FIG. 2 is a schematic front view illustrating an apparatus for producing a glass sheet of a comparative example.
- FIG. 1 is a schematic front view illustrating an apparatus for producing a glass sheet of the present invention.
- the production apparatus is for producing a glass sheet (glass substrate) for a liquid crystal display by an overflow down-draw method.
- the production apparatus is provided with a forming furnace 11 for forming a glass ribbon B by overflowing a molten glass A supplied to a forming trough 10 having a wedge-shaped cross-section from the top portion of the forming trough 10 and allowing the molten glass A to fuse at the lower end portion of the forming trough 10 , an annealing furnace 12 for removing the internal strain in the glass ribbon B while annealing the glass ribbon B, a cooling chamber 13 for sufficiently cooling the glass ribbon B annealed, and a cutting chamber 14 for cutting the glass ribbon B cooled in a given size.
- the cooling chamber 13 is provided with a gas exhausting passage 15 at its ceiling portion.
- the forming furnace 11 and the annealing furnace 12 are surrounded by a forming chamber 16 .
- the cooling chamber 13 and the forming chamber 16 are communicated with each other via the gas exhausting passage 15 .
- the cooling chamber 13 , the cutting chamber 14 , and the forming chamber 16 which are neighboring in the vertical direction, are surrounded by a peripheral wall portion 17 having airtightness.
- the forming furnace 11 , the annealing furnace 12 , the cooling chamber 13 , and the cutting chamber 14 are communicated with each other via a conveyance passage 18 through which the glass ribbon B flows down.
- the cutting chamber 14 is provided with another conveyance passage for conveying a glass sheet C to a subsequent step (for example, edge-polishing step) which is not shown.
- the molten glass A is first supplied to the top portion of the forming trough 10 provided in the forming furnace 11 , the molten glass A is caused to overflow from the top portion of the forming trough 10 , and the molten glass A is fused at the lower end portion of the forming trough 10 , to thereby form into a sheet-like glass ribbon B.
- a pair of cooling rollers (edge rollers) 19 are provided, and the cooling rollers 19 hold both edges of the glass ribbon B, thereby suppressing its contraction in the width direction to a minimum extent.
- annealing the formed glass ribbon B in the annealing furnace 12 removes its internal strain.
- the annealing furnace 12 is provided with a plurality of pairs of pulling rollers (annealing roller) 19 in the vertical direction, and the glass ribbon B is pulled downward while the pulling rollers 20 are pulling the glass ribbon B in the width direction to prevent the glass ribbon B from contracting in the width direction because of surface tension or the like.
- the annealing furnace 12 is set so as to have a given temperature gradient controlled by a heater (not shown). Thus, the temperature of the glass ribbon B is gradually lowered as the glass ribbon B flows down through the annealing furnace 12 , thereby removing the internal strain.
- the cooling chamber 13 in the downstream of the annealing furnace 12 is provided with a plurality of pairs of supporting rollers 21 , which pull downward the glass ribbon B solidified in a given width and given thickness.
- the glass ribbon B is cooled to around room temperature in the cooling chamber 13 .
- the air in the cooling chamber 13 flows into both the annealing furnace 12 and the gas exhausting passage 15 , and the air that has flown into the gas exhausting passage 15 flows into the forming chamber 16 .
- the amount of the air flowing into the annealing furnace 12 is reduced, suppressing the climb of the low-temperature airflow in the conveyance passage 18 of the glass ribbon.
- the glass ribbon cooled to around room temperature in the cooling chamber 14 is cut into glass sheets C having a given size in the cutting chamber 14 , and the glass sheets are conveyed to a subsequent step.
- the above-mentioned apparatus for producing a glass sheet was used to form a glass sheet for a liquid crystal display containing, in terms of mass %, 60% of SiO 2 , 15% of Al 2 O 3 , 10% of B 2 O 3 , 6% of CaO, 6% of SrO, 2% of BaO, and 1% of an fining agent (OA-10, manufactured by Nippon Electric Glass Co., Ltd.).
- the dimension of the glass sheet obtained was 2360 ⁇ 2030 ⁇ 0 0.7 mm.
- the maximum strain of the glass sheet was measured and was 0.8 MPa.
- FIG. 2 is a schematic front view illustrating an apparatus for producing a glass sheet of a comparative example.
- the structure of the apparatus is the same as that of the apparatus in FIG. 1 except that a cooling chamber 13 is not provided with a gas exhausting passage.
- the apparatus in FIG. 2 was used to produce a glass sheet in the same conditions as those in the above-mentioned embodiment.
- the maximum strain of the glass sheet was measured and was 1.1 MPa.
- the glass sheet obtained in the embodiment has a smaller maximum strain than the glass sheet obtained in the comparative example, and hence the present invention has a greater effect of reducing the internal strain of a glass sheet by providing a gas exhausting passage leading from the cooling chamber to a chamber surrounding the annealing furnace.
- the maximum strain of a glass sheet was determined by measuring strain stress from the birefringence amount of the glass sheet through an optical heterodyne interferometry with a strain indicator manufactured by Uniopt Co., Ltd.
- the reason why the maximum strain of a glass sheet was determined is that if even only one strong strain is present in the glass sheet, the glass sheet does not meet the product specification for a glass sheet for a liquid crystal display.
- the present invention is not limited to the above-mentioned embodiment, and may be carried out in any other various embodiments as long as the embodiments do not deviate from the gist of the present invention.
- the above-mentioned embodiment described the case where the present invention was applied to the production of a glass sheet by an overflow down-draw method.
- the present invention can be likewise applied to the production of a glass sheet by a slot down-draw method.
- the forming furnace and the annealing furnace may be each surrounded by different chambers (for example, forming chamber and annealing chamber).
- the gas exhausting passage of the cooling chamber is provided so as to lead to the annealing chamber.
- the gas exhausting passage may be provided apart from the annealing furnace.
- the shape and size of the gas exhausting passage be suitably set depending on the size of the cooling chamber and annealing furnace or the like.
- the process and apparatus for producing a glass sheet of the present invention can be used for the production, mainly of a glass sheet for a liquid crystal display, of a glass sheet used for various flat panel displays, for example, a plasma display, an electroluminescence display such as an OLED display, and a field emission display, and of a glass sheet used as a substrate on which various devices with an electronic display function or various thin films are formed.
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- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
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- Re-Forming, After-Treatment, Cutting And Transporting Of Glass Products (AREA)
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JP2007-331304 | 2007-12-25 | ||
JP2007331304 | 2007-12-25 | ||
JP2008276565A JP5428287B2 (ja) | 2007-12-25 | 2008-10-28 | ガラス板の製造方法及び製造設備 |
JP2008-276565 | 2008-10-28 | ||
PCT/JP2008/072451 WO2009081741A1 (ja) | 2007-12-25 | 2008-12-10 | ガラス板の製造方法及び製造設備 |
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US20100281920A1 US20100281920A1 (en) | 2010-11-11 |
US8322161B2 true US8322161B2 (en) | 2012-12-04 |
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US12/810,173 Active 2029-03-06 US8322161B2 (en) | 2007-12-25 | 2008-12-10 | Process and apparatus for producing glass sheet |
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US (1) | US8322161B2 (zh) |
JP (1) | JP5428287B2 (zh) |
KR (1) | KR101518984B1 (zh) |
CN (1) | CN101815680B (zh) |
TW (1) | TWI422539B (zh) |
Cited By (2)
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US20140130649A1 (en) * | 2012-11-09 | 2014-05-15 | Chester Hann Huei Chang | Methods of processing a glass ribbon |
US10737962B2 (en) | 2015-02-04 | 2020-08-11 | Corning Incorporated | System for forming a glass article |
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JP4621996B2 (ja) * | 2007-04-24 | 2011-02-02 | 日本電気硝子株式会社 | ガラス板製造方法およびガラス板製造設備 |
CN102574721B (zh) | 2010-09-30 | 2013-09-25 | 安瀚视特股份有限公司 | 玻璃板的制造方法 |
JP5669006B2 (ja) * | 2010-10-19 | 2015-02-12 | 日本電気硝子株式会社 | 帯状ガラスフィルム製造方法及び帯状ガラスフィルム製造装置 |
US9676650B2 (en) * | 2011-03-28 | 2017-06-13 | Avanstrate Inc. | Method and apparatus for making glass sheet |
TWI417255B (zh) * | 2011-06-30 | 2013-12-01 | Avanstrate Inc | A manufacturing method of a glass plate and a manufacturing apparatus for a glass plate |
CN103204630B (zh) * | 2011-07-01 | 2020-06-09 | 安瀚视特控股株式会社 | 平面显示器用玻璃基板及其制造方法 |
US8794036B2 (en) * | 2011-08-23 | 2014-08-05 | Corning Incorporated | Apparatus and method for separating a glass sheet from a moving ribbon of glass |
KR101346939B1 (ko) * | 2011-09-29 | 2014-01-03 | 아반스트레이트코리아 주식회사 | 글라스판의 제조 방법 및 글라스판 제조 장치 |
US9598301B2 (en) | 2011-11-29 | 2017-03-21 | Corning Incorporated | Temperature control of glass ribbons during forming |
CN105377786B (zh) * | 2013-09-03 | 2018-10-26 | 日本电气硝子株式会社 | 玻璃及其制造方法 |
CN105264284B (zh) * | 2013-09-03 | 2018-04-06 | 日本电气硝子株式会社 | 导光板 |
US9758418B1 (en) * | 2016-04-06 | 2017-09-12 | Corning Incorporated | Methods of producing glass ribbon |
WO2020068463A1 (en) * | 2018-09-25 | 2020-04-02 | Corning Incorporated | Glass manufacturing apparatus and methods |
CN114555536B (zh) * | 2019-12-18 | 2024-02-13 | 日本电气硝子株式会社 | 玻璃物品的制造方法以及玻璃物品的制造装置 |
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US20140130649A1 (en) * | 2012-11-09 | 2014-05-15 | Chester Hann Huei Chang | Methods of processing a glass ribbon |
US9216924B2 (en) * | 2012-11-09 | 2015-12-22 | Corning Incorporated | Methods of processing a glass ribbon |
US9822028B2 (en) | 2012-11-09 | 2017-11-21 | Corning Incorporated | Methods of processing a glass ribbon |
US10737962B2 (en) | 2015-02-04 | 2020-08-11 | Corning Incorporated | System for forming a glass article |
Also Published As
Publication number | Publication date |
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TWI422539B (zh) | 2014-01-11 |
JP2009173524A (ja) | 2009-08-06 |
TW200934735A (en) | 2009-08-16 |
KR20100100745A (ko) | 2010-09-15 |
CN101815680A (zh) | 2010-08-25 |
JP5428287B2 (ja) | 2014-02-26 |
US20100281920A1 (en) | 2010-11-11 |
CN101815680B (zh) | 2012-11-28 |
KR101518984B1 (ko) | 2015-05-11 |
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